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US4132672A
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Methanation catalyst
Assignee: American Gas Association Inc
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Filing: 1977-02-23
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Granted: 1979-01-02
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Expires: 1997-02-23
Abstract
Abstract An improved method for the conversion of hydrogen and carbon monoxide to a methane-rich gas in which there is employed a supported nickel catalyst promoted by the addition of a small percentage of the iridium metal, typically 0.1 to 1.0% by weight. Said promoted catalyst is highly active for methanation and has good resistance against poisoning by sulfur compounds.
Inventors
- 👤 Henry Wise
- 👤 Bernard Wood
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 07:33
CPC Classifications
C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; C07C1/0435; B; B01; B01J; B01J23/00; B01J23/70; B01J23/89; B01J23/892; C07C1/0445; C07C2521/00; C07C2521/02; C07C2521/04; C07C2523/00; C07C2523/38; C07C2523/40; C07C2523/46; C07C2523/70; C07C2523/74; C07C2523/755; C07C2523/89
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
108 words
A catalyst for the conversion of carbon monoxide and hydrogen to methane consisting essentially of a porous alumina support carrying about 25 percent by weight of metallic nickel catalyst together with from about 0.1 to about 1 percent by weight of iridium, said catalyst having been prepared by depositing the metallic nickel catalyst on the alumina support, impregnating the supported metallic nickel catalyst with an aqueous solution of a water soluble salt of iridium, converting said salt to metallic iridium, and heating the resulting catalyst at a temperature of from about 350° to about 500° C. in the presence of hydrogen for about 4 to about 20 hours.
Claim 2
Dependent Claim
108 words
A catalyst for the conversion of carbon monoxide and hydrogen to methane consisting essentially of a porous alumina support carrying about 25 percent by weight of metallic nickel catalyst together with from about 0.1 to about 1 percent by weight of iridium, said catalyst having been prepared by depositing the metallic nickel catalyst on the alumina support, impregnating the supported metallic nickel catalyst with an aqueous solution of a water soluble salt of iridium, converting said salt to metallic iridium, and heating the resulting catalyst at a temperature of from about 350° to about 500° C. in the presence of hydrogen for about 4 to about 20 hours.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-01-01 | 1982-07-03 | 1983-01-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-01 | 1986-07-03 | 1987-01-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-01 | 1990-07-03 | 1991-01-02 | $7700.00 | Window Closed / Lapsed |